EP0957065A2 - Aluminiumsilikatsuspension - Google Patents
Aluminiumsilikatsuspension Download PDFInfo
- Publication number
- EP0957065A2 EP0957065A2 EP99109070A EP99109070A EP0957065A2 EP 0957065 A2 EP0957065 A2 EP 0957065A2 EP 99109070 A EP99109070 A EP 99109070A EP 99109070 A EP99109070 A EP 99109070A EP 0957065 A2 EP0957065 A2 EP 0957065A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- aluminum silicate
- suspension
- aluminum
- stirring
- aqueous
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
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Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B33/00—Silicon; Compounds thereof
- C01B33/20—Silicates
- C01B33/26—Aluminium-containing silicates, i.e. silico-aluminates
Definitions
- the invention relates to an aqueous Aluminum silicate suspension, a process for its Manufacture and its use.
- Aluminum silicate such as P 820
- P 820 is described in Ullmann's Encyclopedia of Chemical Engineering, 4. Edition, volume 21, page 467, table 12. It is called Bulk filler used in papermaking.
- Aluminum silicate can reduce the printability of newsprint and thin printing paper can be improved.
- Aluminum silicate is a white powder contained in this Form is distributed.
- the aluminum silicate therefore has the disadvantage that separate for its use in papermaking Devices for processing on the basis of powdery consistency can be built and used have to. This disadvantage can be overcome if that Aluminum silicate powder in the form of an aqueous suspension can be used in paper production.
- the invention relates to an aqueous Aluminum silicate suspension, which characterized is that, in addition to water, it is preferred at least 30% by weight at least 35% by weight, aluminum silicate, 0.1 to 3.0% by weight Contains aluminum sulfate and 0.1 to 5.0 wt .-% surfactants.
- Aluminum silicate the aluminum silicate P 820 is used become.
- Nonionic surfactants such as Example polyethylene oxide can be used.
- Anionic and / or cationic surfactants are used.
- Such surfactants are, for example, polyacrylates, dodecylbenzenesulfonate, Sodium citrate.
- the solids content of the suspension can be in one preferred embodiment 35 to 45% by weight, in particular 35 to 40 wt .-%.
- the pH of the suspension can between 4.5 and 9.5, preferably between 5.0 and 8.0, lie.
- Another object of the invention is a method for Production of the aluminum silicate suspension, which thereby is characterized in that an aluminum silicate synthetic way from aluminum sulfate and water glass fails and filtered off, the aluminum silicate filter cake with stirring and / or shearing with an aqueous Liquefied aluminum sulfate solution, at least one surfactant adds to the liquefied Aluminum silicate filter cake with stirring and / or scissors powdered aluminum silicate adds and the mixture if necessary, stir and / or shear again.
- the Wash and dry the aluminum silicate filter cake In one embodiment of the invention, the Wash and dry the aluminum silicate filter cake.
- the aluminum silicate powder obtained can be stirred and / or scissors with an aqueous aluminum sulfate solution mix, add at least one surfactant to this Suspension with stirring and / or scissors more Add powdered aluminum silicate and the mixture if necessary stir and / or shear again.
- the aqueous aluminum silicate suspension according to the invention advantageously has a high solids content. Sedimentation of the solid occurs even with one longer storage time.
- a grinding for destructuring is not necessary.
- the aqueous aluminum silicate suspension according to the invention can be used in papermaking.
- the starting materials are characterized in Table 1: Physico-chemical data of P 820A powder and filter cake P 820A powder P 820 A filter cake Ramming density [g / l] 237 - Loss on drying [%] 6.4 70.0 Solids content [%] 93.6 30th average grain size [ ⁇ m] 5.6 7.5 Surface [m 2 / g] 66 - DBP adsorption [g / 100 g] 90 - PH value 9.5 8.9 (slurry)
- Aluminum sulfate PH value Viscosity [mPa * s] [ml solution] [g / 100g slurry] 0 0 8.9 2000 0.5 0.02 8.9 2000 2nd 0.09 8.2 1800 4th 0.18 6.8 1600 6 0.27 6.1 1500 8th 0.36 5.7 1430 10th 0.45 5.3 1400 12th 0.54 5.1 1500 14 0.63 4.9 1900 16 0.72 4.8 1650 18th 0.81 4.6 1650 20th 0.90 4.5 1450 25th 1.13 4.4 1200 Shear time [min] Viscosity [mPa * s] average particle size d 50 [ ⁇ m] 0 2600 7.7 5 100 7.1 10th 80 7.1 15 65 7.1 20th 55 7.1
- the surfactant additive is at low speed stirred in. After that, the suspension is at 8500 for one minute U / min dispersed. The amount added is in the tables 5 to 7 specified.
- the autoconcentration time is 15 minutes.
- the so suspension obtained is at 3000 for a further 30 min U / min dispersed.
- the sample bottles are placed upside down in the vibrating sieve (Fa. Retsch, AS 200 digit) clamped and with amplitude 100 with Interval shaken. There will be time until the suspensions are completely redispersed. If no Redispersion can be achieved, the experiment after 10 min canceled.
- Fra. Retsch AS 200 digit
- the liquefied suspension is on the magnetic stirrer for 5 min mixed up. After switching off the stirrer, the pH value read.
- the Viscosity measured with the Brookfield DV-II + (spindle no. 62, 100 RPM). Here, too, the value is read after 5 minutes.
- the grain size of the Suspension determined with the grindometer.
- 100 g of the redispersed suspension are in Drying cabinet at 105 ° C to constant weight dried.
- the suspensions are liquid after production, but become pasty when cooling. This can also be done through the Addition of the examined additives cannot be prevented. However, the suspensions are very different in the amount of energy required to liquefy it can be done. It tries to do this necessary Energy input through a defined shaking or turning of the sample glass. With some samples thereby liquefaction can be achieved. But there is also suspensions caused by just shaking and turning are not to be liquefied, but do so immediately after pierce the suspension surface with a spatula becomes. Therefore, for the assessment of the Redispersibility all observations taken together and subjectively a scale from very good to very bad assigned. The results are in Table 4 listed.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
- Paper (AREA)
- Colloid Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
Description
Physikalisch-chemische Daten von P 820A-Pulver und Filterkuchen | ||
P 820A Pulver | P 820 A Filterkuchen | |
Stampfdichte [g/l] | 237 | - |
Trockenverlust [%] | 6,4 | 70,0 |
Feststoffgehalt [%] | 93,6 | 30 |
mittlere Korngröße [µm] | 5,6 | 7,5 |
Oberfläche [m2/g] | 66 | - |
DBP-Adsorption [g/100 g] | 90 | - |
pH-Wert | 9,5 | 8,9 (Slurry) |
Alumuniumsulfat | pH-Wert | Viskosität [mPa*s] | |
[ml Lösung] | [g/100g Slurry] | ||
0 | 0 | 8,9 | 2000 |
0,5 | 0,02 | 8,9 | 2000 |
2 | 0,09 | 8,2 | 1800 |
4 | 0,18 | 6,8 | 1600 |
6 | 0,27 | 6,1 | 1500 |
8 | 0,36 | 5,7 | 1430 |
10 | 0,45 | 5,3 | 1400 |
12 | 0,54 | 5,1 | 1500 |
14 | 0,63 | 4,9 | 1900 |
16 | 0,72 | 4,8 | 1650 |
18 | 0,81 | 4,6 | 1650 |
20 | 0,90 | 4,5 | 1450 |
25 | 1,13 | 4,4 | 1200 |
Scherzeit [min] | Viskosität [mPa*s] | mittlere Teilchengröße d 50 [µm] |
0 | 2600 | 7,7 |
5 | 100 | 7,1 |
10 | 80 | 7,1 |
15 | 65 | 7,1 |
20 | 55 | 7,1 |
Beurteilung der verschiedenen Stabilisatoren | |||
Stabilisator | Einarbeitbarkeit | Sedimentationsverhalten | Redispergierbarkeit |
Polyethylenoxid | |||
Polyacrylat (MG = 1.200) | |||
Polyacrylat (MG = 8.000) | |||
Polyacrylat (MG = 15.000) | |||
Natrimcitrat | |||
EDTA | |||
Polyethylenglykol (MG = 200) | |||
Polyethylenglykol (MG = 2.000) | |||
Polyethylenglykol (MG = 10.000) | |||
Dodecylbenzolsulfonat |
Claims (4)
- Wäßrige Aluminiumsilikatsuspension, dadurch gekennzeichnet, daß sie neben Wasser mindestens 30 Gew.-% Aluminiumsilikat, 0,1 bis 3,0 Gew.-% Aluminiumsulfat und 0,1 bis 5,0 Gew.-% Tensid enthält.
- Verfahren zur Herstellung der Aluminiumsilikatsuspension nach Anspruch 1, dadurch gekennzeichnet, daß man ein Aluminiumsilikat auf synthetischem Wege aus Aluminiumsulfat und Wasserglas ausfällt und abfiltriert, den Aluminiumsilikatfilterkuchen unter Rühren und/oder Scheren mit einer wäßrigen Aluminiumsulfatlösung verflüssigt, mindestens ein Tensid hinzufügt, zu dem verflüssigten Aluminiumsilikatfilterkuchen unter Rühren und/oder Scheren pulverförmiges Aluminiumsilikat hinzugibt und die Mischung gegebenenfalls ein weiteres Mal rührt und/oder schert.
- Verfahren zur Herstellung der Aluminiumsilikatsuspension nach Anspruch 2, dadurch gekennzeichnet, daß man den Aluminiumsilikatfilterkuchen wäscht und trocknet, das erhaltene Aluminiumsilikatpulver unter Rühren und/oder Scheren mit einer wäßrigen Aluminiumsulfatlösung vermischt, mindestens ein Tensid hinzufügt, zu dieser Suspension unter Rühren und/oder Scheren weiteres Aluminiumsilikatpulver hinzufügt und die Mischung gegebenenfalls ein weiteres Mal rührt und/oder schert.
- Verwendung der Aluminiumsilikatsuspension bei der Herstellung von Papier.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19821143 | 1998-05-12 | ||
DE19821143A DE19821143A1 (de) | 1998-05-12 | 1998-05-12 | Aluminiumsilikatsuspension |
Publications (3)
Publication Number | Publication Date |
---|---|
EP0957065A2 true EP0957065A2 (de) | 1999-11-17 |
EP0957065A3 EP0957065A3 (de) | 2000-05-03 |
EP0957065B1 EP0957065B1 (de) | 2003-09-17 |
Family
ID=7867463
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP99109070A Expired - Lifetime EP0957065B1 (de) | 1998-05-12 | 1999-05-07 | Aluminiumsilikatsuspension |
Country Status (7)
Country | Link |
---|---|
US (1) | US6207721B1 (de) |
EP (1) | EP0957065B1 (de) |
AT (1) | ATE250008T1 (de) |
DE (2) | DE19821143A1 (de) |
DK (1) | DK0957065T3 (de) |
ES (1) | ES2205630T3 (de) |
TW (1) | TW546253B (de) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6207721B1 (en) | 1998-05-12 | 2001-03-27 | Degussa-Huls Aktiengesellschaft | Aluminum silicate suspension |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB0013406D0 (en) * | 2000-06-02 | 2000-07-26 | Crosfield Joseph & Sons | Zeolite compositions and their use |
AU2004225819B2 (en) * | 2003-04-02 | 2008-08-21 | Ciba Specialty Chemicals Water Treatments Limited | Aqueous compositions and their use in the manufacture of paper and paperboard |
US11518893B2 (en) * | 2018-11-20 | 2022-12-06 | Columbia Insurance Company | Manufacturing method for multi paint finishes and a multi-finish extender grind |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0046171A1 (de) * | 1980-08-16 | 1982-02-24 | Hoechst Aktiengesellschaft | Lagerstabile und fliessfähige wässrige Suspensionen von Natriumaluminiumsilicaten |
FR2628341A1 (fr) * | 1988-03-09 | 1989-09-15 | Rhone Poulenc Chimie | Suspension aqueuse stable de silico-aluminates |
GB2245262A (en) * | 1990-06-22 | 1992-01-02 | Unilever Plc | Aluminosilicate slurries l |
Family Cites Families (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CA815971A (en) * | 1969-06-24 | Nauroth Peter | Process for producing sodium aluminium silicate pigments | |
US3130063A (en) * | 1961-03-23 | 1964-04-21 | Huber Corp J M | Stabilization of fluid suspensions of filler grade clay |
US3582379A (en) * | 1968-05-21 | 1971-06-01 | Huber Corp J M | Alkali metal alumino silicates,methods for their production and compositions thereof |
US4122031A (en) * | 1971-06-24 | 1978-10-24 | Anglian Water Authority | Complex alkali metal-metal silicate material |
AT335035B (de) * | 1974-10-10 | 1977-02-25 | Henkel & Cie Gmbh | Stabile suspensionen wasserunloslicher, zum binden von calciumionen befahigter silikate und deren verwendung zur herstellung von wasch- und reinigungsmitteln |
US4169075A (en) | 1974-10-10 | 1979-09-25 | Henkel Kommanditgesellschaft Auf Aktien | Process for the production of powdery washing agents by spray-drying |
JPS5155114A (en) * | 1974-11-08 | 1976-05-14 | Nitto Chemical Industry Co Ltd | Doshitsuno anteikaho |
DE2615698A1 (de) * | 1976-04-09 | 1977-10-20 | Henkel & Cie Gmbh | Stabile suspensionen wasserunloeslicher, zum binden von calciumionen befaehigter silikate und deren verwendung zur herstellung von wasch- und reinigungsmitteln |
DE2727475C2 (de) * | 1977-06-18 | 1983-06-23 | Degussa Ag, 6000 Frankfurt | Verfahren zur Herstellung von tensidhaltigen, kationenaustauschenden Alumosilikaten |
GB2015488B (en) * | 1978-03-02 | 1982-09-22 | Unilever Ltd | Stabilised sodium aluminosilicate suspensions |
BE874420A (fr) | 1978-03-02 | 1979-08-23 | Unilever Nv | Procede de production de compositions detergentes |
DE3021295C2 (de) * | 1980-06-06 | 1986-10-16 | Basf Ag, 6700 Ludwigshafen | Wäßrige lagerstabile, fließ- und pumpfähige Natriumalumosilikat-Suspensionen |
US5648055A (en) * | 1992-05-26 | 1997-07-15 | E. I. Du Pont De Nemours And Company | Method for preparing low-concentration polyaluminosilicate microgels |
DE69414571T2 (de) * | 1993-06-01 | 1999-06-17 | Akzo Pq Silica Vof | Verfahren zur herstellung von aluminosilikat für aufzeichnungsmaterial |
US5482693A (en) * | 1994-03-14 | 1996-01-09 | E. I. Du Pont De Nemours And Company | Process for preparing water soluble polyaluminosilicates |
US5786077A (en) * | 1995-06-07 | 1998-07-28 | Mclaughlin; John R. | Anti-slip composition for paper |
DE19821143A1 (de) | 1998-05-12 | 1999-11-18 | Degussa | Aluminiumsilikatsuspension |
-
1998
- 1998-05-12 DE DE19821143A patent/DE19821143A1/de not_active Ceased
-
1999
- 1999-05-06 TW TW088107402A patent/TW546253B/zh not_active IP Right Cessation
- 1999-05-07 DK DK99109070T patent/DK0957065T3/da active
- 1999-05-07 ES ES99109070T patent/ES2205630T3/es not_active Expired - Lifetime
- 1999-05-07 DE DE59906985T patent/DE59906985D1/de not_active Expired - Fee Related
- 1999-05-07 AT AT99109070T patent/ATE250008T1/de not_active IP Right Cessation
- 1999-05-07 EP EP99109070A patent/EP0957065B1/de not_active Expired - Lifetime
- 1999-05-10 US US09/307,754 patent/US6207721B1/en not_active Expired - Fee Related
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0046171A1 (de) * | 1980-08-16 | 1982-02-24 | Hoechst Aktiengesellschaft | Lagerstabile und fliessfähige wässrige Suspensionen von Natriumaluminiumsilicaten |
FR2628341A1 (fr) * | 1988-03-09 | 1989-09-15 | Rhone Poulenc Chimie | Suspension aqueuse stable de silico-aluminates |
GB2245262A (en) * | 1990-06-22 | 1992-01-02 | Unilever Plc | Aluminosilicate slurries l |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6207721B1 (en) | 1998-05-12 | 2001-03-27 | Degussa-Huls Aktiengesellschaft | Aluminum silicate suspension |
Also Published As
Publication number | Publication date |
---|---|
EP0957065B1 (de) | 2003-09-17 |
DE19821143A1 (de) | 1999-11-18 |
US6207721B1 (en) | 2001-03-27 |
ATE250008T1 (de) | 2003-10-15 |
DK0957065T3 (da) | 2004-01-26 |
ES2205630T3 (es) | 2004-05-01 |
DE59906985D1 (de) | 2003-10-23 |
TW546253B (en) | 2003-08-11 |
EP0957065A3 (de) | 2000-05-03 |
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